WO2019054119A1 - 複合半透膜及びその製造方法 - Google Patents

複合半透膜及びその製造方法 Download PDF

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WO2019054119A1
WO2019054119A1 PCT/JP2018/030437 JP2018030437W WO2019054119A1 WO 2019054119 A1 WO2019054119 A1 WO 2019054119A1 JP 2018030437 W JP2018030437 W JP 2018030437W WO 2019054119 A1 WO2019054119 A1 WO 2019054119A1
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Prior art keywords
semipermeable membrane
composite semipermeable
skin layer
polyfunctional
porous support
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PCT/JP2018/030437
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English (en)
French (fr)
Japanese (ja)
Inventor
倫次 宮部
井上　真一
友葉 岡▲崎▼
知哉 小川
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日東電工株式会社
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Application filed by 日東電工株式会社 filed Critical 日東電工株式会社
Priority to EP18857259.8A priority Critical patent/EP3682964A4/en
Priority to US16/645,642 priority patent/US20200261860A1/en
Priority to KR1020207010415A priority patent/KR102551961B1/ko
Priority to CN201880058948.9A priority patent/CN111050891A/zh
Publication of WO2019054119A1 publication Critical patent/WO2019054119A1/ja

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    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D69/00—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
    • B01D69/12—Composite membranes; Ultra-thin membranes
    • B01D69/125—In situ manufacturing by polymerisation, polycondensation, cross-linking or chemical reaction
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D67/00—Processes specially adapted for manufacturing semi-permeable membranes for separation processes or apparatus
    • B01D67/0002—Organic membrane manufacture
    • B01D67/0006—Organic membrane manufacture by chemical reactions
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D67/00—Processes specially adapted for manufacturing semi-permeable membranes for separation processes or apparatus
    • B01D67/0081—After-treatment of organic or inorganic membranes
    • B01D67/0093—Chemical modification
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D69/00—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
    • B01D69/02—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor characterised by their properties
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D69/00—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
    • B01D69/06—Flat membranes
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D69/00—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
    • B01D69/10—Supported membranes; Membrane supports
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D69/00—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
    • B01D69/12—Composite membranes; Ultra-thin membranes
    • B01D69/1213—Laminated layers
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D69/00—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
    • B01D69/12—Composite membranes; Ultra-thin membranes
    • B01D69/125—In situ manufacturing by polymerisation, polycondensation, cross-linking or chemical reaction
    • B01D69/1251—In situ manufacturing by polymerisation, polycondensation, cross-linking or chemical reaction by interfacial polymerisation
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D71/00—Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor
    • B01D71/06—Organic material
    • B01D71/56—Polyamides, e.g. polyester-amides
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2323/00—Details relating to membrane preparation
    • B01D2323/12—Specific ratios of components used
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2323/00—Details relating to membrane preparation
    • B01D2323/40—Details relating to membrane preparation in-situ membrane formation
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2325/00—Details relating to properties of membranes
    • B01D2325/20—Specific permeability or cut-off range
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2325/00—Details relating to properties of membranes
    • B01D2325/30—Chemical resistance
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/08—Seawater, e.g. for desalination
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/10—Nature of the water, waste water, sewage or sludge to be treated from quarries or from mining activities

Definitions

  • the present invention relates to a composite semipermeable membrane comprising a skin layer and a porous support for supporting the same, and a method for producing the same.
  • a composite semipermeable membrane is suitable for the production of ultrapure water, desalination of brackish water or seawater, etc., and is a contamination source contained in contaminations or the like that are causes of pollution such as dyeing drainage and electrodeposition paint drainage.
  • the active substance can be removed and recovered to contribute to the closing of the drainage.
  • it can be used for advanced treatment such as concentration of active ingredients in food applications and removal of harmful components in water purification and sewage applications. It can also be used for wastewater treatment in oil fields and shale gas fields.
  • the composite semipermeable membrane is called RO (reverse osmosis) membrane, NF (nanofiltration) membrane, FO (forward osmosis) membrane depending on its filtration performance and treatment method, and ultrapure water production, seawater desalination, removal of brine It can be used for salt treatment, waste water reuse treatment, etc.
  • a skin layer containing a polyamide-based resin formed by reacting a polyfunctional amine component and a polyfunctional acid halide component is formed on the surface of a porous support
  • Composite semipermeable membranes can be mentioned.
  • the composite semipermeable membrane is required to have stable water separation performance.
  • water eg, sewage
  • the contaminants eg, microorganisms
  • the quality of raw water varies widely in wastewater treatment etc., and the number of times of cleaning tends to increase.
  • a solution containing an oxidizing agent is often used for cleaning the composite semipermeable membrane, but cleaning the composite semipermeable membrane with a solution containing the oxidizing agent degrades the composite semipermeable membrane and the water treatment performance fluctuates significantly. There was a problem.
  • Patent Document 1 a composite semipermeable membrane having oxidation resistance (chlorine resistance), for example, a composite semipermeable membrane using piperazine as a multifunctional amine component is known (Patent Document 1).
  • Patent Document 1 Although the composite semipermeable membrane of Patent Document 1 is excellent in oxidant resistance (chlorine resistance), there is a problem that the salt rejection rate is low.
  • Patent Document 2 discloses a semipermeable composite membrane having a porous support membrane and an ultrathin film composed mainly of a crosslinked polypiperazine amide obtained by an interfacial reaction.
  • a technique has been proposed in which the ultrathin film is brought into contact with a chlorine-containing aqueous solution at pH 1.0 to 10 at normal pressure.
  • An object of the present invention is to provide a composite semipermeable membrane excellent in oxidizing agent resistance (chlorine resistance) and salt blocking property and a method for producing the same.
  • the present invention is a composite semipermeable membrane in which a skin layer containing a polyamide resin obtained by polymerizing a polyfunctional amine component and a polyfunctional acid halide component is formed on the surface of a porous support,
  • the polyfunctional amine component comprises an alicyclic diamine
  • FT-IR Fastier transform infrared spectroscopy
  • the skin layer is a very thin film, and it is very difficult to specify its thickness, the relationship between the thickness of the skin layer and the water separation performance of the composite semipermeable membrane has been studied so far. It was not.
  • the inventor of the present invention has found that, instead of the thickness of the skin layer, the C of the amide group of the polyamide based resin which is the material for forming the skin layer obtained by the transmission method of FT-IR (Fourier transform infrared spectroscopy).
  • the absorption peak intensity derived from O stretching vibration was employed as an index, and it was found that there is a correlation between the absorption peak intensity and the salt rejection of the composite semipermeable membrane.
  • the composite semipermeable membrane having the skin layer having the absorption peak intensity of 0.03 or more is very excellent in the salt blocking property as compared with the conventional composite semipermeable membrane.
  • the absorption peak intensity of the skin layer of the conventional composite semipermeable membrane is about 0.01 to 0.02.
  • the absorption peak intensity is preferably 0.1 or less from the viewpoint of securing practical water permeability.
  • the alicyclic diamine is preferably a heteroalicyclic diamine in which the hetero atom constituting the ring is nitrogen, from the viewpoint of being excellent in oxidation resistance (chlorine resistance), and piperazine is more preferable. preferable.
  • the polyamide resin is preferably chlorinated in the range of 0.1 to 7% from the viewpoint of improving the salt blocking property.
  • the polyfunctional acid halide component is preferably trimesic acid trichloride from the viewpoint of improving the salt blocking property.
  • a skin layer containing a polyamide resin is brought into contact with the surface of the porous support by bringing an amine solution containing a polyfunctional amine component into contact with an organic solution containing a polyfunctional acid halide component on the porous support.
  • a process for producing a composite semipermeable membrane comprising the steps of:
  • the polyfunctional amine component comprises an alicyclic diamine
  • the amine solution relates to a method for producing a composite semipermeable membrane characterized in that it contains 3% by weight or more of the polyfunctional amine component.
  • a composite semipermeable membrane having a skin layer having an absorption peak intensity of 0.03 or more can be manufactured.
  • the skin layer of the composite semipermeable membrane of the present invention is formed using an alicyclic diamine as a polyfunctional amine component, and the absorption peak intensity is 0.03 or more. Not only is excellent in oxidation resistance (chlorine resistance), but also has excellent salt blocking properties as compared with conventional composite semipermeable membranes.
  • the composite semipermeable membrane of the present invention is used, the operation amount of water treatment becomes easy because the amount of water permeation hardly changes even if the washing is repeated with the solution containing the oxidizing agent.
  • a skin layer containing a polyamide resin is formed on the surface of a porous support, and the skin layer is transparent to FT-IR (Fourier transform infrared spectroscopy).
  • FT-IR Fastier transform infrared spectroscopy
  • the polyamide resin is obtained by polymerizing a polyfunctional amine component and a polyfunctional acid halide component.
  • alicyclic diamines are used as the polyfunctional amine component.
  • the alicyclic diamine is not particularly limited.
  • diaminocyclohexane such as 1,3-diaminocyclohexane, 1,2-diaminocyclohexane, and 1,4-diaminocyclohexane
  • piperazine substituted by an alkyl group having 1 to 2 carbon atoms
  • Piperazine eg, 2-methylpiperazine, 2-ethylpiperazine, 2,5-dimethylpiperazine, 2,5-diethylpiperazine, etc.
  • 4-aminomethylpiperazine eg, 2-methylpiperazine, 2-ethylpiperazine, 2,5-dimethylpiperazine, 2,5-diethylpiperazine, etc.
  • the heteroalicyclic diamine whose hetero atom which comprises rings, such as a compound represented, is nitrogen is mentioned.
  • n is an integer of 1 to 3.
  • hydrogen bonded to a carbon atom constituting a ring has 1 to 2 carbon atoms
  • It may be substituted by an alkyl group.
  • aromatic polyfunctional amines include m-phenylenediamine, p-phenylenediamine, o-phenylenediamine, 1,3,5-triaminobenzene, 1,2,4-triaminobenzene, 3,5-diamino
  • aromatic polyfunctional amines include m-phenylenediamine, p-phenylenediamine, o-phenylenediamine, 1,3,5-triaminobenzene, 1,2,4-triaminobenzene, 3,5-diamino
  • examples thereof include benzoic acid, 2,4-diaminotoluene, 2,6-diaminotoluene, N, N'-dimethyl-m-phenylenediamine, 2,4-diaminoanisole, amidol, and xylylenediamine. These may be used alone or in combination of two or more.
  • aliphatic polyfunctional amines examples include ethylenediamine, propylenediamine, tris (2-aminoethyl) amine, and N-phenyl-ethylenediamine. These may be used alone or in combination of two or more.
  • the said alicyclic diamine and the said aromatic or aliphatic polyfunctional amine it is preferable to use 85 weight% or more of the said alicyclic diamine in the whole polyfunctional amine component, More preferably, it is 90 weight% It is the above, More preferably, it is 95 weight% or more.
  • the polyfunctional acid halide component is a polyfunctional acid halide having two or more reactive carbonyl groups.
  • Polyfunctional acid halides include aromatic, aliphatic and alicyclic polyfunctional acid halides.
  • aromatic polyfunctional acid halides include trimesic acid trichloride, terephthalic acid dichloride, isophthalic acid dichloride, biphenyldicarboxylic acid dichloride, naphthalenedicarboxylic acid dichloride, benzenetrisulfonic acid trichloride, benzenedisulfonic acid dichloride, and chlorosulfonylbenzene.
  • Dicarboxylic acid dichloride etc. are mentioned.
  • aliphatic polyfunctional acid halides examples include propanedicarboxylic acid dichloride, butanedicarboxylic acid dichloride, pentanedicarboxylic acid dichloride, propanetricarboxylic acid trichloride, butanetricarboxylic acid trichloride, pentanetricarboxylic acid trichloride, glutaryl halide, and azide. Poil halide etc. are mentioned.
  • alicyclic polyfunctional acid halides include cyclopropane tricarboxylic acid trichloride, cyclobutane tetracarboxylic acid tetrachloride, cyclopentane tricarboxylic acid trichloride, cyclopentane tetracarboxylic acid tetrachloride, cyclohexane tricarboxylic acid trichloride, and tetrahydrofuran.
  • Examples thereof include tetracarboxylic acid tetrachloride, cyclopentanedicarboxylic acid dichloride, cyclobutanedicarboxylic acid dichloride, cyclohexanedicarboxylic acid dichloride, and tetrahydrofurandicarboxylic acid dichloride.
  • polyfunctional acid halides may be used alone or in combination of two or more.
  • an aromatic polyfunctional acid halide it is preferable to use an aromatic polyfunctional acid halide.
  • a polymer such as polyvinyl alcohol, polyvinyl pyrrolidone, or polyacrylic acid; a polyhydric alcohol such as sorbitol or glycerin may be coated.
  • the porous support for supporting the skin layer is not particularly limited as long as it can support the skin layer.
  • materials for forming the porous support include various materials such as polysulfone, polyarylethersulfone such as polyethersulfone, polyimide, poly (vinylidene fluoride) and the like, but chemical, mechanical and thermal ones are particularly preferable. Polysulfone and polyarylether sulfone are preferably used in view of their stability.
  • the thickness of such porous support is usually, but not necessarily limited to, about 25 to 125 ⁇ m, preferably about 40 to 75 ⁇ m.
  • the porous support may be reinforced by backing with a base material such as woven fabric or non-woven fabric.
  • the porous support may have a symmetric structure or an asymmetric structure, but an asymmetric structure is preferable from the viewpoint of achieving both the support function of the skin layer and the liquid permeability.
  • the average pore diameter of the skin layer-forming side surface of the porous support is preferably 0.01 to 0.5 ⁇ m.
  • an epoxy resin porous sheet may be used as the porous support.
  • the average pore diameter of the porous epoxy resin sheet is preferably 0.01 to 0.4 ⁇ m.
  • the method for forming the skin layer containing the polyamide resin on the surface of the porous support is not particularly limited, and any known method can be used.
  • an interfacial condensation method, a phase separation method, a thin film coating method and the like can be mentioned.
  • a skin layer is formed by contacting an amine solution containing a polyfunctional amine component with an organic solution containing a polyfunctional acid halide component to form a skin layer, and the skin layer And a method of directly forming a skin layer of a polyamide based resin on the porous support by the interfacial polymerization on the porous support.
  • the details of the conditions and the like of the interfacial condensation method are described in JP-A-58-24303, JP-A-1-180208 and the like, and those known techniques can be appropriately adopted.
  • an amine solution coating layer composed of an amine solution containing the alicyclic diamine is formed on a porous support, and then an organic solution containing a polyfunctional acid halide component is brought into contact with the amine solution coating layer. It is preferable to form a skin layer by interfacial polymerization.
  • Examples of the solvent of the amine solution include water; alcohols such as ethylene glycol, isopropyl alcohol, and ethanol; and mixed solvents of these alcohols and water.
  • the concentration of the polyfunctional amine component in the amine solution is 3% by weight or more, preferably 5% by weight or more, more preferably 7% by weight or more, and still more preferably 9% by weight or more It is. If the concentration of the polyfunctional amine component is less than 3% by weight, it is not possible to form a skin layer having an absorption peak intensity of 0.03 or more. On the other hand, when the concentration of the polyfunctional amine component in the amine solution is too high, the absorption peak intensity of the obtained skin layer becomes too high, and the permeation resistance tends to be increased and the water permeability tends to be lowered. Therefore, the concentration of the polyfunctional amine component is preferably 11% by weight or less, more preferably 10% by weight or less.
  • the concentration of the polyfunctional acid halide component in the organic solution is not particularly limited, but is preferably 0.1 to 5% by weight, more preferably 0.1 to 3% by weight, and still more preferably 0.1 ⁇ 2 wt%.
  • concentration of the polyfunctional acid halide component is less than 0.1% by weight, it becomes difficult to form a skin layer having an absorption peak intensity of 0.03 or more.
  • concentration of the polyfunctional acid halide component exceeds 5% by weight, the unreacted polyfunctional acid halide component tends to remain easily, or the absorption peak intensity of the obtained skin layer becomes too large, resulting in permeation resistance. And the permeability tends to decrease.
  • the organic solvent used in the organic solution is not particularly limited as long as it has low solubility in water, does not degrade the porous support, and dissolves the polyfunctional acid halide component, and examples thereof include cyclohexane, heptane, and octane. And saturated hydrocarbons such as nonane, and halogen-substituted hydrocarbons such as 1,1,2-trichlorotrifluoroethane. It is preferably a saturated hydrocarbon having a boiling point of 300 ° C. or less, more preferably 200 ° C. or less, a naphthenic solvent, or an isoparaffinic solvent.
  • the organic solvents may be used alone or in combination of two or more.
  • additives may be added to the amine solution or the organic solution for the purpose of facilitating membrane formation or improving the performance of the resulting composite semipermeable membrane.
  • the additive include surfactants such as sodium dodecyl benzene sulfonate, sodium dodecyl sulfate, and sodium lauryl sulfate, sodium hydroxide which removes hydrogen halide generated by polymerization, trisodium phosphate, triethylamine and the like.
  • the heating temperature is more preferably 70 to 200 ° C., particularly preferably 100 to 150 ° C.
  • the heating time is preferably about 30 seconds to 10 minutes, and more preferably about 40 seconds to 7 minutes.
  • the absorption peak intensity is preferably 0.1 or less, more preferably 0.09 or less, from the viewpoint of securing practical water permeability.
  • the reagent used for the chlorination treatment is not particularly limited, and examples thereof include: chlorine gas, alkali metal salts of hypochlorite such as sodium chloride powder, sodium hypochlorite, chlorine dioxide, chloramine B, chloramine T, harazone, dichlorodimethylhydantoin, Chlorinated isocyanuric acid and salts thereof and the like can be mentioned. It is preferable to use an aqueous solution of sodium hypochlorite having a pH of 1 to 10 from the viewpoint of ease of chlorination of polyamide resin and handleability.
  • hypochlorite such as sodium chloride powder, sodium hypochlorite, chlorine dioxide, chloramine B, chloramine T, harazone, dichlorodimethylhydantoin, Chlorinated isocyanuric acid and salts thereof and the like can be mentioned. It is preferable to use an aqueous solution of sodium hypochlorite having a pH of 1 to 10 from the viewpoint of ease of chlorination of polyamide resin and handleability
  • the method of chlorination treatment is not particularly limited.
  • a method of immersing the skin layer in the treatment liquid a method of applying or spraying the treatment liquid on the skin layer, a method of pressurizing and passing the treatment liquid to the skin layer, etc. It can be mentioned.
  • the method of passing the treatment liquid under pressure through the skin layer is preferable.
  • the concentration of the aqueous solution of sodium hypochlorite is about 5 to 100 ppm (preferably 5 to 40 ppm), and the operating pressure at the time of pressure passing is 0.5 to It is about 2.0 MPa.
  • the polyamide resin in the skin layer is preferably chlorinated at a chlorination rate of 0.1 to 7%, more preferably 0.5 to 4.0%, by chlorination treatment. Preferably, it is 1.0 to 3.0%. If the chlorination rate is less than 0.1%, the effect of improving the salt inhibition by chlorination can not be sufficiently obtained. On the other hand, when the chlorination rate exceeds 7%, the salt rejection rate tends to decrease.
  • the composite semipermeable membrane in order to improve the salt blocking property, the water permeability, the oxidation resistance and the like of the composite semipermeable membrane, conventionally known various treatments may be performed.
  • a dry semi-permeable composite membrane may be used from the viewpoint of excellent processability and storage stability.
  • the composite semipermeable membrane of the present invention is not limited in its shape. That is, any conceivable membrane shape is possible, such as a flat membrane or a spiral element.
  • the salt rejection ratio was calculated in advance by using the correlations (calibration curves) of NaCl concentration and aqueous solution conductivity and using them.
  • Salt inhibition rate (%) ⁇ 1- (NaCl concentration in permeate [mg / L]) / (NaCl concentration in feed solution [mg / L]) ⁇ ⁇ 100
  • the produced composite semipermeable membrane was immersed in cyclohexanone to dissolve the porous polysulfone support, and the skin layer containing the polyamide resin was isolated.
  • a resin such as polyvinyl alcohol may be applied to the surface of the skin layer in advance in order to prevent the skin layer from cracking and tearing.
  • the isolated skin layer was washed three times with cyclohexanone and once with ethanol.
  • the skin layer was laminated on the PET film so as to cover the hole having a diameter of 1 cm provided in the PET film (thickness: about 180 ⁇ m) with the skin layer, and the skin layer was dried at room temperature for 30 minutes to prepare a measurement sample .
  • a measurement sample is attached to a Fourier transform infrared spectrophotometer (PerkinElmer, Spectrum TWO), and scanning is performed in a range of 700 to 4000 cm -1 by a transmission method of FT-IR (Fourier transform infrared spectroscopy).
  • Chlorination ratio (%) ⁇ (Cl element ratio ⁇ Na element ratio) / (N element ratio / 2) ⁇ ⁇ 100
  • Example 1 An aqueous amine solution containing 7% by weight of piperazine, 0.15% by weight of sodium dodecyl sulfate, 1.48% by weight of sodium hydroxide and 6% by weight of camphorsulfonic acid is coated on a porous polysulfone support (asymmetric membrane), Thereafter, the aqueous solution coating layer was formed by removing excess aqueous amine solution. Next, the surface of the aqueous solution coating layer was immersed for 10 seconds in an acid chloride solution in which 0.42% by weight of trimesic acid trichloride (TMC) was dissolved in an isoparaffinic solvent (IP 1016, manufactured by Idemitsu Kosan Co., Ltd.).
  • TMC trimesic acid trichloride
  • Example 2 The composite semipermeable membrane prepared in Example 1 is set in a cell for flat membrane evaluation, pH 7.5, an aqueous solution containing 20 ppm of sodium hypochlorite is applied at 1.5 MPa to the feed side and the permeate side of the composite semipermeable membrane. Differential pressure was applied to make contact for 30 minutes to chlorinate the polyamide resin in the skin layer.
  • Example 3 A composite semipermeable membrane was produced in the same manner as in Example 2 except that the piperazine concentration in the aqueous amine solution was changed to 3% by weight.
  • Example 4 A composite semipermeable membrane was produced in the same manner as in Example 2 except that the piperazine concentration in the aqueous amine solution was changed to 9% by weight.
  • Example 5 A composite semipermeable membrane was produced in the same manner as in Example 2 except that the concentration of sodium hypochlorite was changed to 80 ppm.
  • Comparative Example 1 A composite semipermeable membrane was produced in the same manner as in Example 2 except that the piperazine concentration in the aqueous amine solution was changed to 1.5% by weight.
  • Comparative example 2 A composite semipermeable membrane was produced in the same manner as in Example 1 except that the piperazine concentration in the aqueous amine solution was changed to 1.5% by weight. Then, the produced composite semipermeable membrane was immersed in an aqueous solution containing pH 7.5 and 700 ppm of sodium hypochlorite at normal pressure for 5 minutes to chlorinate the polyamide resin in the skin layer.
  • the composite semipermeable membrane of the present invention is suitable for the production of ultrapure water, desalination of brackish water or seawater, etc., and is included in contamination due to pollution such as dyeing drainage and electrodeposition paint drainage. It is possible to remove and recover the contaminated sources or effective substances and contribute to the closing of the drainage. In addition, it can be used for advanced treatment such as concentration of active ingredients in food applications and removal of harmful components in water purification and sewage applications. It can also be used for wastewater treatment in oil fields and shale gas fields.

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Organic Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)
PCT/JP2018/030437 2017-09-15 2018-08-16 複合半透膜及びその製造方法 WO2019054119A1 (ja)

Priority Applications (4)

Application Number Priority Date Filing Date Title
EP18857259.8A EP3682964A4 (en) 2017-09-15 2018-08-16 SEMIPERMEABLE COMPOSITE MEMBRANE AND METHOD OF MANUFACTURING THEREOF
US16/645,642 US20200261860A1 (en) 2017-09-15 2018-08-16 Composite semipermeable membrane and method for manufacturing same
KR1020207010415A KR102551961B1 (ko) 2017-09-15 2018-08-16 복합 반투막 및 그의 제조 방법
CN201880058948.9A CN111050891A (zh) 2017-09-15 2018-08-16 复合半透膜及其制造方法

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2023176049A1 (ja) * 2022-03-14 2023-09-21 日東電工株式会社 複合逆浸透膜及びその製造方法
WO2023176048A1 (ja) * 2022-03-14 2023-09-21 日東電工株式会社 複合逆浸透膜及びその製造方法

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US11167249B2 (en) * 2015-07-31 2021-11-09 Toray Industries, Inc. Separation membrane, separation membrane element, water purifier, and method for producing separation membrane

Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5824303A (ja) 1981-08-03 1983-02-14 Teijin Ltd 耐酸化性複合半透膜
JPS63123406A (ja) 1986-11-13 1988-05-27 Toray Ind Inc 半透性複合膜の製造方法
US4769148A (en) 1987-11-18 1988-09-06 The Dow Chemical Company Novel polyamide reverse osmosis membranes
JPH01180208A (ja) 1988-01-11 1989-07-18 Toray Ind Inc 複合半透膜の製造方法およびその膜
JPH08224452A (ja) 1994-12-22 1996-09-03 Nitto Denko Corp 高透過性複合逆浸透膜の製造方法
JP2010137192A (ja) * 2008-12-15 2010-06-24 Toray Ind Inc 複合ナノろ過膜
JP2014233652A (ja) * 2013-05-31 2014-12-15 東レ株式会社 複合半透膜
WO2015114727A1 (ja) * 2014-01-28 2015-08-06 日東電工株式会社 複合分離膜とこれを用いた分離膜エレメント
JP2016093797A (ja) * 2014-11-17 2016-05-26 日東電工株式会社 複合分離膜とこれを用いた分離膜エレメント

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CA2087421A1 (en) * 1992-01-22 1993-07-23 Hisao Hachisuka Composite reverse osmosis membrane and novel acid chloride
US20030136727A1 (en) * 1999-05-27 2003-07-24 Hideki Yamada Composite semipermeable membrane
JP2001286741A (ja) * 2000-04-04 2001-10-16 Toray Ind Inc 逆浸透複合膜およびその製造方法
US6337018B1 (en) * 2000-04-17 2002-01-08 The Dow Chemical Company Composite membrane and method for making the same
CN104487160B (zh) * 2012-07-19 2018-11-23 陶氏环球技术有限责任公司 结构改善的复合聚酰胺膜

Patent Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5824303A (ja) 1981-08-03 1983-02-14 Teijin Ltd 耐酸化性複合半透膜
JPS63123406A (ja) 1986-11-13 1988-05-27 Toray Ind Inc 半透性複合膜の製造方法
US4769148A (en) 1987-11-18 1988-09-06 The Dow Chemical Company Novel polyamide reverse osmosis membranes
JPH01180208A (ja) 1988-01-11 1989-07-18 Toray Ind Inc 複合半透膜の製造方法およびその膜
JPH08224452A (ja) 1994-12-22 1996-09-03 Nitto Denko Corp 高透過性複合逆浸透膜の製造方法
JP2010137192A (ja) * 2008-12-15 2010-06-24 Toray Ind Inc 複合ナノろ過膜
JP2014233652A (ja) * 2013-05-31 2014-12-15 東レ株式会社 複合半透膜
WO2015114727A1 (ja) * 2014-01-28 2015-08-06 日東電工株式会社 複合分離膜とこれを用いた分離膜エレメント
JP2016093797A (ja) * 2014-11-17 2016-05-26 日東電工株式会社 複合分離膜とこれを用いた分離膜エレメント

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2023176049A1 (ja) * 2022-03-14 2023-09-21 日東電工株式会社 複合逆浸透膜及びその製造方法
WO2023176048A1 (ja) * 2022-03-14 2023-09-21 日東電工株式会社 複合逆浸透膜及びその製造方法

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